Cooking method for pulp
a technology of lignocellulose and cooking method, which is applied in the field of effective cooking method of lignocellulose material, can solve the problems of no research or development on the type of quinone compound that is effective for cooking and improvemen
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example 1
(1) Preparation of a polysulfide cooking liquor
[0042]A two compartment electrolytic cell was assembled, which comprised a nickel plate as an anode current collector, a nickel foam as an anode (100 mm×20 mm×4 mm, average pore diameter of network: 0.51 mm, surface area of the anode per volume of the anode compartment: 5,600 m2 / m3, surface area to the diaphragm area: 28 m2 / m2), an iron expansion metal as a cathode and a fluororesin type cation exchange membrane as a diaphragm. The anode compartment had a height of 100 mm, a width of 20 mm and a thickness of 4 mm, and the cathode compartment had a height of 100 mm, a width of 20 mm and a thickness of 5 mm. The effective area of the diaphragm was 20 cm2. Using model white liquor, circulation electrolysis was carried out at an anode solution linear velocity of 4 cm / sec. at a current density of 6 kA / m2 at an electrolysis temperature of 90° C., whereby a polysulfide cooking liquor having the following composition was obtained at a selectivi...
example 2
[0049]Cooking was carried out in the same manner as in Example 1 except that as a quinone compound, tetrahydroanthraquinone (disodium 1,4-dihydro-9,10-dihydroxyanthracene, SAQ, trade name, manufactured by Kawasaki Kasei Chemicals Ltd.) (Ea=0.154V) was added so that it would be the same molar amount as in Example 1. The results of the cooking are shown in Table 1. Like in Example 1, as compared with Comparative Examples 1 and 2, the Kappa number at the same active alkali addition decreased, and the yield of pulp at the same Kappa number increased.
example 3
[0050]Cooking was carried out in the same manner as in Example 1 except that as a quinone compound, 2-methyl-9,10-anthraquinone (Ea=0.154V) was added so that it would be the same molar amount as in Example 1. The results of the cooking are shown in Table 1. Like in Example 1, as compared with Comparative Examples 1 and 2, the Kappa number at the same active alkali addition decreased, and the yield of pulp at the same Kappa number increased.
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